KINETIC CALCULATION OF PLASMA-AIR AND PLASMA-STEAM GASIFICATION OF SOLID FUELS

K. Umbetkaliev, A. Ustimenko
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Abstract

In this paper, kinetic calculation of kuchekinsky coal plasma-air and plasma-steam gasification in a cylindrical channels with plasma source is performed. For kinetic calculations one-dimensional kinetic code Plasma-Coal were applied. Calculation results showed that gas phase in plasma-air gasification products, starting from the coordinate value of 0.15 m, is mainly represented by synthesis gas, concentration of which at reactor outlet is 48.6%. At the same time, the concentration of carbon monoxide over the entire temperature range is higher than the concentration of hydrogen. Their concentration at reactor outlet is 31.2% and 17.5%, respectively. Gas phase of plasma-steam gasification products is also represented mainly by synthesis gas. At 0.15 m reactor length, synthesis gas concentration is 93.9%, and reached up to 100% at reactor outlet.
固体燃料等离子体-空气和等离子体-蒸汽气化动力学计算
本文对库切金斯基煤等离子体-空气和等离子体-蒸汽在圆柱形通道内的气化动力学进行了计算。动力学计算采用一维动力学程序等离子体-煤。计算结果表明,等离子体-空气气化产物中的气相从坐标值0.15 m开始,以合成气为主,反应器出口的合成气浓度为48.6%。同时,在整个温度范围内一氧化碳的浓度高于氢的浓度。它们在反应器出口的浓度分别为31.2%和17.5%。等离子体-蒸汽气化产物气相也以合成气为主。当反应器长度为0.15 m时,合成气浓度为93.9%,在反应器出口达到100%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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